CN205635515U - Coalescence operation filter equipment - Google Patents
Coalescence operation filter equipment Download PDFInfo
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- CN205635515U CN205635515U CN201620392729.2U CN201620392729U CN205635515U CN 205635515 U CN205635515 U CN 205635515U CN 201620392729 U CN201620392729 U CN 201620392729U CN 205635515 U CN205635515 U CN 205635515U
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- container
- defecator
- coalescence
- low head
- shell
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Abstract
The utility model relates to a coalescence operation filter equipment, characterized by: at least, include: fast open -blind board shell, container low head, fast open -blind board shell and the container low head interface in proper order formation sealed container that meets, the container low head is located on the skirt, cut apart it become container and lower container in the central level of shell by separating the chamber board, upward the container top water is kept flat and has been put the clamp plate, the clamp plate and separate the chamber board between connect a plurality of coalescent filter perpendicularly, the lower container lateral wall have terminal wire mesh mist catcher, natural gas import is in last container lateral wall, natural gas export is in the lower container lateral wall, the drain has outwards been drawn forth to container low head bottom. The device makes the coalescence of natural gas gas -liquid, gravity and terminal interception function in an organic whole to guarantee the absorption tower and give vent to anger moisturely up to standard, reduce the running cost.
Description
Technical field
This utility model relates to a kind of natural gas filter, particularly a kind of coalescence operation defecator.
Technical background
The natural gas of extraction from stratum, because of pressure, variations in temperature, has substantial amounts of saturated solution and separates out, these saturated solutions
Exceeded a certain amount of after, to downstream 2,2'-ethylenedioxybis(ethanol). dehydration bring the biggest pressure, time serious will cause 2,2'-ethylenedioxybis(ethanol). dehydration after natural
Air water dew point is the most up to standard, directly affects product quality and downstream user uses.At present, the front end of 2,2'-ethylenedioxybis(ethanol). dewatering process flow is provided only with
Gravity separator, this gravity separator can only carry out the separation of big drop, it is impossible to deviates from saturated solution.Traditional three are sweet
Alcohol air inlet flow process: carry out gas and be introduced into gravity separator, enters 2,2'-ethylenedioxybis(ethanol). absorption tower after carrying out simple Gravity Separation, inhales through 2,2'-ethylenedioxybis(ethanol).
After receipts, gas transports to user as outside product gas.Owing in the gas on entrance absorption tower, liquid content is relatively big, three circulated in absorption tower
Glycol can not fully absorb moisture, causes the water dew point in product gas the most up to standard；Give vent to anger aqueous up to standard sometimes for guarantee, must not
Strengthen the circulating load of 2,2'-ethylenedioxybis(ethanol). the most at double, thus cause operating cost to increase.
Summary of the invention
The purpose of this utility model is to provide a kind of coalescence operation defecator, in order to make the coalescence of natural gas gas-liquid, gravity
And end interception function is in one, thus it is aqueous up to standard to ensure to give vent to anger in absorption tower, reduces operating cost.
The purpose of this utility model is achieved in that a kind of coalescence operation defecator, it is characterized in that: at least include:
Fast opening blind shell, container low head；Fast opening blind shell and container low head interface successively connect to being formed and seal
Container；Container low head is seated on skirt；It is divided into upper container and lower appearance by separate space plate in shell central horizontal
Device；Upper container top horizontal is placed with pressing plate；The multiple Coalescence filter cores of vertical connection between pressing plate and separate space plate；Described lower container
Sidewall has end wire-mesh mist extractor；Imported gas is at described upper container sidewall, and gas outlet is in described lower container side
Wall；Sewage draining exit is outwards led to bottom container low head.
Described upper container sidewall has drain.
Described upper container has differential manometer upper interface, described lower container to have differential manometer lower interface.
Described lower container side wall has liquid level mouth on liquidometer.
Liquid level mouth under liquidometer is outwards drawn bottom described container low head.
Described upper container sidewall has gauge port.
Described separate space plate lower end connects downspout, and downspout is vertically downward.
Described interval, multiple Coalescence filter cores portion in a reservoir is uniformly distributed concentrically justifies.
Described end wire-mesh mist extractor or horizontally disposed, or be arranged vertically.
Described separate space plate and shell or be welded to connect, or bolt adds and is tightly connected.
The utility model has the advantages that: owing to carrying out gas through Imported gas containing saturated solution, enter intracavity on shell
Portion first carries out Gravity Separation, and the liquid that Gravity Separation goes out drains into shell cavity of resorption by downspout；Sky after Gravity Separation
So gas enters Coalescence filter core, then is coalesced by the filtering layer that Coalescence filter core is special, and droplet saturated in gas is agglomerated into big drop,
The big drop formed flows into shell cavity of resorption along the inner tube wall of Coalescence filter core, from Coalescence filter core inner core natural gas via end out
After end wire-mesh mist extractor intercepts, then discharged by gas outlet, enter 2,2'-ethylenedioxybis(ethanol). absorption tower, natural gas gas-liquid can be made to coalesce,
Gravity and end interception function are in one, thus it is aqueous up to standard to ensure to give vent to anger in absorption tower, reduces operating cost.
Accompanying drawing explanation
Below in conjunction with embodiment, the utility model is described in further detail:
Fig. 1 is that this utility model embodiment one coalesces operation filter apparatus configuration sketch；
Fig. 2 is the A-A generalized section of Fig. 1.
In figure, 1, skirt, 2, liquid level mouth under liquidometer, 3, container low head, 4, downspout, 5, liquid level mouth on liquidometer,
6, differential manometer lower interface, 7, separate space plate, 8, differential manometer lower interface, 9, Coalescence filter core, 10, shell, 11, natural gas enters
Mouthful, 12, pressing plate, 13, fast opening blind, 14, gauge port, 15, drain, 16, gas outlet, 17, end wire-mesh mist extractor,
18, sewage draining exit.
Detailed description of the invention
Embodiment 1
A kind of coalescence operation defecator, is characterized in that: at least include: seal under fast opening blind 13 shell 10, container
3；Fast opening blind 13 shell 10 and container low head 3 interface successively connect to being formed and seal container；Container low head 3 is located
On skirt 1；It is divided into upper container and lower container by separate space plate 7 in shell 10 central horizontal；Upper container top water
Keep flat and be equipped with pressing plate 12；The multiple Coalescence filter cores 9 of vertical connection between pressing plate 12 and separate space plate 7；Described lower container side wall has end
End wire-mesh mist extractor 17；Imported gas 11 is at described upper container sidewall, and gas outlet 16 is at described lower container side wall；
Sewage draining exit 18 is outwards led to bottom container low head 3.
Embodiment 2
As depicted in figs. 1 and 2, a kind of coalescence operation defecator: at least include: fast opening blind 13 shell 10, appearance
Device low head 3；Fast opening blind 13 shell 10 and container low head 3 interface successively connect to being formed and seal container；Seal under container
3 are seated on skirt 1；It is divided into upper container and lower container by separate space plate 7 in shell 10 central horizontal；Upper container
Top horizontal is placed with pressing plate 12；The multiple Coalescence filter cores 9 of vertical connection between pressing plate 12 and separate space plate 7；Described lower container side
Wall has end wire-mesh mist extractor 17；Imported gas 11 is at described upper container sidewall, and gas outlet 16 is in described lower appearance
Device sidewall；Sewage draining exit 18 is outwards led to bottom container low head 3.Drain 15, differential manometer top is had to connect at upper container sidewall
Mouth 8, upper container sidewall have gauge port 14.Liquid level mouth 5 on differential manometer lower interface 6, liquidometer is had at lower container side wall.
Liquid level mouth 2 under liquidometer is outwards drawn bottom described container low head 3.
Described separate space plate 7 lower end connects downspout 4, and downspout 4 is vertically downward.
Described interval, multiple Coalescence filter cores portion in a reservoir is uniformly distributed concentrically justifies.
End wire-mesh mist extractor 17 or horizontally disposed, or be arranged vertically.
Described separate space plate 7 and shell 10 or be welded to connect, or bolt adds and is tightly connected.
Separation process of the present utility model is: carry out gas through Imported gas 11 containing saturated solution, enters on shell 10
Intracavity portion first carries out Gravity Separation, and the liquid that Gravity Separation goes out drains into shell 10 cavity of resorption by downspout 4；Through Gravity Separation
After natural gas enter Coalescence filter core 9, then coalesced by the special filtering layer of Coalescence filter core, droplet saturated in gas be agglomerated into
Big drop, the big drop of formation flows into shell 10 cavity of resorption, from Coalescence filter core 9 inner core out along the inner tube wall of Coalescence filter core 9
Natural gas via end wire-mesh mist extractor 17 intercept after, then discharged by gas outlet 16, enter 2,2'-ethylenedioxybis(ethanol). absorption tower.
Parts that the present embodiment describes the most in detail and structure belong to the well-known components of the industry and common structure or conventional hands
Section, describes the most one by one.
Claims (10)
1. a coalescence operation defecator, is characterized in that: at least include: under fast opening blind (13) shell (10), container
End socket (3)；Fast opening blind (13) shell (10) and container low head (3) interface successively connect to being formed and seal container；Container
Low head (3) is seated on skirt (1)；Shell (10) central horizontal by separate space plate (7) be divided into upper container and
Lower container；Upper container top horizontal is placed with pressing plate (12)；Vertical connection multiple coalescence filter between pressing plate (12) and separate space plate (7)
Core (9)；Described lower container side wall has end wire-mesh mist extractor (17)；Imported gas (11) at described upper container sidewall,
Gas outlet (16) is at described lower container side wall；Container low head (3) bottom outwards leads to sewage draining exit (18).
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described upper container sidewall has emptying
Mouth (15).
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described upper container has on differential manometer
Portion's interface (8), described lower container has differential manometer lower interface (6).
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described lower container side wall has liquid level
Liquid level mouth (5) on meter.
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described container low head (3) end
Liquid level mouth (2) under liquidometer are outwards drawn in portion.
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described upper container sidewall has pressure
Table mouth (14).
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described separate space plate (7) lower end is even
Being connected to downspout (4), downspout (4) is vertically downward.
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described multiple Coalescence filter cores are holding
In the middle part of device, interval is uniformly distributed and concentrically justifies.
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described end wire-mesh mist extractor
Or horizontally disposed, or be arranged vertically (17).
A kind of coalescence operation defecator the most according to claim 1, is characterized in that: described separate space plate (7) and container
Cylinder (10) or be welded to connect, or bolt adds and is tightly connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620392729.2U CN205635515U (en) | 2016-05-04 | 2016-05-04 | Coalescence operation filter equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620392729.2U CN205635515U (en) | 2016-05-04 | 2016-05-04 | Coalescence operation filter equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205635515U true CN205635515U (en) | 2016-10-12 |
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ID=57050191
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620392729.2U Active CN205635515U (en) | 2016-05-04 | 2016-05-04 | Coalescence operation filter equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205635515U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260853A (en) * | 2018-11-21 | 2019-01-25 | 沈阳鑫联石化设备有限公司 | A kind of boat coal filter separator |
-
2016
- 2016-05-04 CN CN201620392729.2U patent/CN205635515U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260853A (en) * | 2018-11-21 | 2019-01-25 | 沈阳鑫联石化设备有限公司 | A kind of boat coal filter separator |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |